JPH05508819A - polyhydroxy acid film - Google Patents
polyhydroxy acid filmInfo
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- JPH05508819A JPH05508819A JP91512895A JP51289591A JPH05508819A JP H05508819 A JPH05508819 A JP H05508819A JP 91512895 A JP91512895 A JP 91512895A JP 51289591 A JP51289591 A JP 51289591A JP H05508819 A JPH05508819 A JP H05508819A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
- B29C55/005—Shaping by stretching, e.g. drawing through a die; Apparatus therefor characterised by the choice of materials
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
- C08G63/06—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C71/00—After-treatment of articles without altering their shape; Apparatus therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0037—Other properties
- B29K2995/0049—Heat shrinkable
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- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Engineering & Computer Science (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Closed-Circuit Television Systems (AREA)
- Two-Way Televisions, Distribution Of Moving Picture Or The Like (AREA)
- Synchronisation In Digital Transmission Systems (AREA)
- Internal Circuitry In Semiconductor Integrated Circuit Devices (AREA)
- Formation Of Insulating Films (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 ポリヒドロキシ酸フィルム 発明の背景 本発明はある種のポリヒドロキシ酸組成物およびこれらの組成物から製造される 、劣化性の包装材料として有用なフィルムに関する。[Detailed description of the invention] polyhydroxy acid film Background of the invention The present invention provides certain polyhydroxy acid compositions and products made from these compositions. , relates to films useful as degradable packaging materials.
ヒドロキシ酸の高分子量ポリマー、およびアルファーヒドロキシ酸特にグリコー ル酸および乳酸のエステル化による環状ダイマー生成物は、劣化性であることが よく知られており、自然環境中に存在する条件または適当な廃棄物処理施設で使 用される条件のもとて実質的にかつ容易に無害の副生成物に劣化する、使い捨て 包装に有用であることがわかっている。High molecular weight polymers of hydroxy acids, and alpha hydroxy acids especially glycols. The cyclic dimer products from esterification of lactic and lactic acids can be degradable. Conditions that are well known and exist in the natural environment or used in suitable waste treatment facilities. Disposable materials that substantially and readily degrade to harmless by-products under the conditions in which they are used. It has been found useful in packaging.
包装材料は、光学的な透明性、引張り強さ、傷に対する耐性および任意的に収縮 性であることを含む、付加的な有益な物理的性質を有することが望ましい。収縮 性のフィルムは、「収縮ラップ」包装に有用である。収縮ラッピングは、それに よっである物質の周囲に配置したフィルム構造が対流熱または輻射熱を加えるこ とにより収縮して、隙間のない、保護用の、自己シール性の容器を与えるための 方法である。ポリヒドロキシ酸フィルムを収縮性にするためには、ポリヒドロキ シ酸フィルムを機械的な延伸処理により配向しなければならない。Packaging materials have optical clarity, tensile strength, scratch resistance and optional shrinkage. It is desirable for the material to have additional beneficial physical properties, including physical properties. contraction Polymer films are useful in "shrink wrap" packaging. shrink wrapping to it Therefore, a film structure placed around a material can add convective or radiant heat. and shrink to provide a tight, protective, self-sealing container. It's a method. To make the polyhydroxy acid film shrinkable, the polyhydroxy acid film must be The silicic acid film must be oriented by a mechanical stretching process.
商業的に重要な多くの高分子量ポリヒドロキシ酸は、大きいな比率の固有の不斉 炭素原子を含み、したがってかなり結晶質で脆いこともある。このようなポリマ ーは、過剰のフィルム破壊なしには、過酷なフィルム形成および配向プロセスに ほとんど耐えることができず、低い収率をもたらす。さらに、かなりの結晶性を 有するポリヒドロキシ酸フィルムは、エージングによって脆くなることもある。Many commercially important high molecular weight polyhydroxy acids have large proportions of inherent chirality. It contains carbon atoms and therefore can be quite crystalline and brittle. Such a polymer - Can withstand harsh film forming and orientation processes without excessive film destruction It is poorly tolerated and results in low yields. Furthermore, considerable crystallinity The polyhydroxy acid film may become brittle with aging.
柔軟なポリヒドロキシ酸フィルムを作る1つの方法は、大量のモノマーのまたは 低分子量オリゴマーのアルファーポリヒドロキシ酸化学種を組み込むことにより 、フィルムを可塑化することである。しかし、このような可塑化されたポリヒド ロキシ酸組成物は、フィルム形成設備にくっつき、不均一な厚さのフィルムを生 じさせ、かつ可塑剤がしばしば設備を汚すため、フィルムに押し出すことが困難 である。フィルムの形態にうまく加工された場合でも、可塑化されたポリヒドロ キシ酸組成物は、それ自身、雰囲気温度に近いガラス転移温度Tgを有し、暖か い気候でみられる保存条件では安定ではない。さらに、可塑化されたポリヒドロ キシ酸組成物は、意図した包装の有効寿命のための構造的な保全性を維持するた めの適当な劣化速度を持つことができず、しかも引き続き収縮性のフィルムに配 向した場合に、製品にうまく付着し良好なパッケージ強度のために要するヒート セット収縮力を示すことができない。One way to make flexible polyhydroxy acid films is to use large amounts of monomer or By incorporating low molecular weight oligomeric alpha polyhydroxy oxidation species , to plasticize the film. However, such plasticized polyhydride Roxy acid compositions can stick to film forming equipment and produce films of non-uniform thickness. Difficult to extrude into film as the plasticizer often contaminates equipment. It is. Even when successfully processed into film form, plasticized polyhydrocarbons The oxyacid composition itself has a glass transition temperature Tg close to ambient temperature, and has a warm temperature. It is not stable under storage conditions found in harsh climates. In addition, plasticized polyhydro The oxy-acid composition is used to maintain structural integrity for the intended useful life of the package. However, if the film is still shrinkable, heat required for good adhesion to the product and good package strength when Unable to show set contraction force.
シュナイダ−(Schne i de r)は、米国特許第2.703,316 号において、乳酸からのフィルムの製造を開示している。シュナイダーの、市販 の乳酸からのポリ乳酸は、本来的にラセミツク(光学不活性)であり、したがっ てそれから製造されたフィルムは、高度に可塑化されたポリヒドロキシ酸組成物 のそれと同様な欠点があるであろう。商業的に有用な、使い捨て包装用途には、 経済的にかつ高い収率で、光学的に透明で丈夫でしかも二軸配向したフィルムに 加工することができる、劣化性の組成物を提供することが望ましい。Schneider, U.S. Patent No. 2.703,316 In issue, the production of film from lactic acid is disclosed. Schneider's commercially available Polylactic acid from lactic acid is inherently racemic (optically inactive) and therefore The films produced therefrom are highly plasticized polyhydroxy acid compositions. It may have the same drawbacks as that of . Commercially useful, single-use packaging applications include: Economically and with high yield, optically clear, durable, and biaxially oriented films can be produced. It is desirable to provide degradable compositions that can be processed.
発明の概要 本発明によれば、以下の工程からなる、劣化性で収縮性のポリマーフィルムの製 造方法が提供される。Summary of the invention According to the present invention, the production of a degradable and shrinkable polymer film consists of the following steps: A manufacturing method is provided.
(a)ポリマー材料を、融液を十分に機械的に撹拌しながら、溶融処理して、以 下の成分を含む均一な組成物を得る:(1)以下から選択される少なくとも1つ のヒドロキシ酸構成部分を含む92から99.9重量%までのポリヒドロキシ酸 ポリマー: (i) (QC口” C00CR’ R” Co) 。(a) Melt-process the polymer material while sufficiently mechanically stirring the melt, and Obtain a homogeneous composition containing the following components: (1) at least one selected from the following: 92 to 99.9% by weight polyhydroxy acid containing a hydroxy acid component of polymer: (i) (QC mouth "C00CR'R" Co).
(百) [0(CR’ R” ) Co]p (山) (OCR’R″CR’R″OCR’又”Co)。(100) [0(CR’R”)Co]p (Mountain) (OCR’R″CR’R″OCR’also”Co).
(i v) (OCR’ R” CR’ R” OCR’ R” CR’ R” Co) 。(iv) (OCR’ R” CR’ R” OCR’ R” CR’ R” Co).
(v) (i) −(iv)と非ヒドロキシ酸コモノマーとのコポリここで、n は2.4または5であり:psqsrおよびSは整数であり、これらの合計は約 350から5,000までの範囲であり、 R1およびRI +は水素、1から 12の炭素原子を含むヒドロカルビル、または1から12の炭素原子を含む置換 ヒドロカルビルであり、自己支持性のフィルムを生じさせるのに十分な分子量を 有する、 (II)モノマーのヒドロキシ酸、モノマーのヒドロキシ酸の環状ダイマー、モ ノマーのヒドロキシ酸の非環状ダイマーおよび分子量450までのモノマーのヒ ドロキシ酸のその他のオリゴマーを含む0.10から8重量%までの可塑剤;( b)この組成物を約0.05から2mmまでの均一な厚さのフィルムに成形する ; (C)こうして製造されたフィルムを、配向をポリヒドロキシ酸のガラス転移温 度より高く組成物の融点よりも低い温度で行い、フィルムをフィルムの最初の機 械方向および横方向の寸法の2倍よりも大きく延伸することにより、二軸配向す る。(v) a copolymer of (i)-(iv) and a non-hydroxy acid comonomer, where n is 2.4 or 5: psqsr and S are integers, and their sum is approximately The range is from 350 to 5,000, R1 and RI + are hydrogen, and 1 to 5,000. Hydrocarbyl containing 12 carbon atoms or substituted containing 1 to 12 carbon atoms is a hydrocarbyl with sufficient molecular weight to produce a self-supporting film. have, (II) Monomeric hydroxy acid, cyclic dimer of monomeric hydroxy acid, acyclic dimers of monomeric hydroxy acids and monomers with molecular weights up to 450. 0.10 to 8% by weight of plasticizers, including other oligomers of droxy acids; ( b) Forming the composition into a film of uniform thickness from about 0.05 to 2 mm. ; (C) The film thus produced is adjusted to the glass transition temperature of the polyhydroxy acid. The film is processed at a temperature higher than 200°C and lower than the melting point of the composition. Biaxially oriented Ru.
また、100℃で5%未満の収縮値を有する、劣化性で非収縮性のポリマーフィ ルムを製造する方法も提供される。Also, a degradable, non-shrinkable polymer fibre, with a shrinkage value of less than 5% at 100°C. A method of manufacturing a lum is also provided.
さらに、前述した方法で作られる物品も提供される。Additionally provided are articles made by the method described above.
発明の詳細な説明 本発明によって製造されるフィルムの劣化性は、ポリヒドロキシ酸の使用によっ て達成される。ここで使用されるように、「ポリヒドロキシ酸」は、以下のもの から選択される少なくとも1つのヒドロキシ酸構成部分を含んでいるポリマーを いう: (’ ) (OCR’ R” C00CR’ R” CO) q(i i) [ 0(CR’ R” ) CO]p (i i i) (OCR’ R” CR’ R” OCR’ R” Co) 。Detailed description of the invention The degradability of the films produced by the present invention is reduced by the use of polyhydroxy acids. achieved. As used herein, "polyhydroxy acid" refers to a polymer containing at least one hydroxy acid moiety selected from say: (’) (OCR’ R” C00CR’ R” CO) q(i i) [ 0(CR’R”)CO]p (i i i) (OCR’ R” CR’ R” OCR’ R” Co) .
l v) (OCR’ R” CR’ R” OCR’ R” CR’ R” CO) 5(v) (i) −(iv)と非ヒドロキシ酸コモノマーとのコポリ ここで、nは2.4または5であり:psqSrおよびSは整数であり、これら の合計は約350から5,000の範囲であり、 R1およびRr rは水素、 1から12の炭素原子を含むヒドロカルビル、または1から12の炭素原子を含 む置換ヒドロカルビルである。l v) (OCR’ R” CR’ R” OCR’ R” CR’ R” CO) 5(v)(i)-(iv) copolymer with non-hydroxy acid comonomer where n is 2.4 or 5: psqSr and S are integers; The sum of is in the range of about 350 to 5,000, and R1 and Rr are hydrogen, hydrocarbyl containing 1 to 12 carbon atoms; or hydrocarbyl containing 1 to 12 carbon atoms; It is a substituted hydrocarbyl.
好適な非ヒドロキシ酸コモノマーの例は、ラクチドまたは乳酸(例えば、イプシ ロン−カプロラクトン、ベータープロピオラクトン、アルファ、アルファージメ チル−ベータープロピオラクトンおよびドデカノラクトンのようなラクトン;ラ クタム;グリコール酸のようなその他のヒドロキシ酸;およびアミノ酸)と縮合 重合できるものを含む。より完全な一覧表のためには、米国特許第4,800, 219号、第9欄、第27行を参照せよ。p、q、rおよびSの値は、配向フィ ルムの製造に適当な結晶化度および結晶化速度を与えるように選択される。Examples of suitable non-hydroxy acid comonomers are lactide or lactic acid (e.g. Ron-caprolactone, beta-propiolactone, alpha, alpha-zime Lactones such as chill-beta propiolactone and dodecanolactone; condensation with other hydroxy acids such as glycolic acid; and amino acids) Including those that can be polymerized. For a more complete listing, see U.S. Patent No. 4,800, See No. 219, column 9, line 27. The values of p, q, r and S are selected to provide a suitable degree of crystallinity and rate of crystallization for the production of lume.
ポリヒドロキシ酸は、ヒドロキシ酸前駆体から直接的に重合によって、またはヒ ドロキシ酸前駆体の環状モノマーまたは環状ダイマーのラクトンの重合によって 合成される。ポリヒドロキシ酸を1つまたはそれ以上のラクトンから製造する場 合には、重合モノマーとしての環状モノマーまたは環状ダイマーの化学種の選択 は、ヒドロキシ酸のタイプに依存するであろう。環状ラクトンからの重合は、中 間体、環状ダイマーおよび低分子量の化学種との平衡反応が、ヒドロキシ酸から 直接的に製造されるポリマーの分子量に実質上の制限を与えるため、高分子量ポ リヒドロキシ酸の製造にとって好ましい。Polyhydroxy acids can be produced by polymerization directly from hydroxy acid precursors or by polymerization. By polymerization of lactones of cyclic monomers or cyclic dimers of droxy acid precursors be synthesized. Where polyhydroxy acids are produced from one or more lactones In this case, the selection of the cyclic monomer or cyclic dimer species as the polymerization monomer will depend on the type of hydroxy acid. Polymerization from cyclic lactones is Equilibrium reactions with intermediates, cyclic dimers, and low molecular weight species occur from hydroxy acids. High molecular weight polymers provide a practical limit to the molecular weight of directly produced polymers. Preferred for the production of hydroxy acids.
本発明のポリヒドロキシ酸は、ポリマー融液から支持できるフィルムを形成する ために十分な粘度および強度を得るのに少なくとも十分高い分子量を有している 。約50,000から約600,000までの範囲の平均分子量;好ましくは約 150,000から約450.000までの平均分子量を有するポリヒドロキシ 酸が本発明には有効である。分子量が高すぎると、組成物を溶融処理するのに要 する温度で、過剰の劣化が起こる。The polyhydroxy acids of the present invention form supportable films from polymer melts. have a molecular weight at least high enough to obtain sufficient viscosity and strength for . Average molecular weight ranging from about 50,000 to about 600,000; preferably about Polyhydroxy having an average molecular weight from 150,000 to about 450,000 Acids are useful in this invention. If the molecular weight is too high, it will be difficult to melt process the composition. Excessive deterioration occurs at temperatures that occur.
ポリヒドロキシ酸に関してここで用いられるように、「劣化性」という用語は、 劣化性の材料のポリヒドロキシ酸部分が生物劣化性であり、かつより重要である が、加水分解により劣化性であることを意味する。劣化速度は、その意図した用 途(例えば、製品は通常の貯蔵および用途ではそれほど劣化しないが、廃棄した 後は妥当な時間で劣化する)に一致する。加水分解劣化のためには、わずかに酸 性または塩基性の条件が有利に用いられる。加水分解劣化の速度は、ポリマー結 晶化度およびさらす水の量によって影響される。加水分解劣化の結果として、有 用なポリヒドロキシ酸への再変換が望まれるならばモノマー単位を回収してもよ いし、モノマー単位を環境的に優しい廃棄物として捨ててもよい。As used herein with respect to polyhydroxy acids, the term "degradable" The polyhydroxy acid moiety of the degradable material is biodegradable and more importantly means that it is degradable by hydrolysis. The rate of deterioration is determined by its intended use. (for example, a product does not deteriorate appreciably with normal storage and use, but if it is discarded) after which it deteriorates in a reasonable amount of time). For hydrolytic degradation, slightly acidic Neutral or basic conditions are advantageously used. The rate of hydrolytic degradation depends on the polymer bond. Affected by crystallinity and amount of water exposed. As a result of hydrolytic deterioration, The monomer units may be recovered if reconversion to a useful polyhydroxy acid is desired. Alternatively, the monomer units may be disposed of as environmentally friendly waste.
「曇った」製品は、一般的に本発明の範囲外であり、低分子量可塑剤のフィルム 表面への押し出し、または出発ポリマーの高い結晶含有量によって引き起こされ る劣った透明性を有する。"Cloudy" products are generally outside the scope of this invention and include films of low molecular weight plasticizers. caused by extrusion to the surface or high crystalline content of the starting polymer It has poor transparency.
「雰囲気温度」という用語は、フィルム製品が使用または貯蔵の間にさらされる であろう最も高い温度をいう。通常、これは冷蔵下での室温(28℃)またはそ れ以下から、倉庫貯蔵での40℃またはそれ以上までの範囲である。The term "ambient temperature" refers to the temperature to which the film product is exposed during use or storage. The highest temperature that will occur. This is usually at room temperature (28°C) or below refrigeration. range from below 40°C to 40°C or above in warehouse storage.
本発明の好ましいポリヒドロキシ酸は、その55−99モル%が Rr が水素 、RI +がメチル基であり、不斉炭素の80−97モル%がR−コンフィギユ レーションおよび3−20モル%がS−コンフィギユレーション、または80− 97モル%がS−コンフィギユレーションおよび3−20モル%がR−コンフィ ギユレーションである、前述した(i)のヒドロキシ酸構成部分からなる主要成 分であり;その1−45モル%が、主要成分および少量成分中の合計のR−また はS−コンフィギユレーションが不斉炭素の97モル%を超えないような不斉炭 素含有量を有する(i)のヒドロキシ酸構成部分、または(iりから(1v)の ヒドロキシ酸のいずれかもしくは適当な非ヒドロキシ酸コモノマーからなる少量 成分であるものである。The preferred polyhydroxy acid of the present invention has 55-99 mol% of which Rr is hydrogen. , RI+ is a methyl group, and 80-97 mol% of the asymmetric carbons are in the R-configuration. and 3-20 mol% S-configuration, or 80- 97 mol% S-configuration and 3-20 mol% R-configuration. The main component consisting of the hydroxy acid component of (i) mentioned above, which is 1-45 mol% of the total R- or is an asymmetric carbon in which the S-configuration does not exceed 97 mol% of the asymmetric carbon. the hydroxy acid moiety of (i) having an elemental content, or (i) of (1v) a small amount of any hydroxy acid or a suitable non-hydroxy acid comonomer It is an ingredient.
好ましいポリヒドロキシ酸は、例えば、不斉炭素の90モル%がS−コンフィギ ユレーションである65モル%のヒドロキシ酸構成部分(1)からなる主要成分 を含んでいてもよい。Preferred polyhydroxy acids include, for example, 90 mol% of the asymmetric carbon atoms in the S-configuration. The main component consists of 65 mol% hydroxy acid component (1) May contain.
この例において、少量成分は、35モル%であり、完全にヒドロキシ酸構成部分 (11)または適当な非ヒドロキシ酸コモノマーからなっていてもよい。この同 じ例において、少量成分は、追加的なヒドロキシ酸構成部分(i)であってもよ いが、少量成分中ではS−コンフィギユレーションである不斉炭素の分率は、主 要成分のS−原子に加えたときに合計のS−原子含有量を97モル%以上に上げ ない分率より大きくなってはならない。In this example, the minor component is 35 mole %, entirely the hydroxy acid component. (11) or a suitable non-hydroxy acid comonomer. This same In the same example, the minor component may be an additional hydroxy acid component (i). However, in the minor components, the fraction of asymmetric carbon in S-configuration is mainly Increases the total S-atom content to 97 mol% or more when added to the S-atoms of essential components. It must not be greater than a fraction that does not exist.
本発明のより好ましい態様においては、ポリヒドロキシ酸の主要成分中のR−お よびS−不斉炭素原子の範囲は85−96モル%であり、主要成分および少量成 分中の合計のR−およびS−不斉炭素原子は96モル%を超えない。In a more preferred embodiment of the present invention, R- or The range of S- and S-asymmetric carbon atoms is 85-96 mol%, with major and minor components. The total R- and S-asymmetric carbon atoms in the portion do not exceed 96 mol%.
「R−」および「S−」という用語は、不斉炭素の立体異性体のコンフィギユレ ーションを同定するための標準的な命名法をいう。ここで示されるR−およびS −炭素のパーセンテージは、ポリマー鎖中の全炭素原子ではなく、ポリマー鎖中 の不斉炭素の分率のみをいう。不斉炭素原子は、それに結合した異なる置換基を 4つも有するものである。The terms "R-" and "S-" refer to stereoisomeric configurations of asymmetric carbon atoms. standard nomenclature for identifying applications. R- and S shown here - The percentage of carbon in the polymer chain, not the total carbon atoms in the polymer chain. refers only to the fraction of asymmetric carbon. An asymmetric carbon atom has different substituents attached to it. It has as many as four.
R−およびS−炭素原子のより対等の分率を含むポリマーは、1)加水分解によ る加速された劣化を示し、かつ2)しばしば互いに接着して隣接した層を有し、 フィルム加工の間に劣化しやすいフィルムを製造するため、好ましい組成物は選 択された不斉炭素原子の狭い範囲を有する。Polymers containing more equal fractions of R- and S-carbon atoms are 1) 2) have adjacent layers that often adhere to each other; Preferred compositions are selected to produce films that are susceptible to degradation during film processing. has a narrow range of asymmetric carbon atoms selected.
また、これらの範囲外のフィルムは、曇っておりおよび/または脆い。例えば、 97%S−炭素原子の範囲を超える分率を有するポリマーフィルムは、フィルム 製造におけるような加熱処理後に実質的に結晶質である。結晶化は、フィルム形 成能、結晶質ポリマーから形成されたフィルムの光学的透明性、および結晶質ポ リマーから延伸により形成されるうまく配向したフィルムができることに対して 有害である。結晶質ポリマーフィルムはまたアモルファスポリマーフィルムより も脆い。高度に結晶質のポリマーの、フィルムの性質へのよくない影響を減らす 方法は、ポリマーマトリクス中にモノマー、低分子量オリゴマーの化学種を組み 込み、分散させることによって、ポリマーを可塑化することである。本発明のポ リヒドロキシ酸に対する可塑剤は、モノマーのヒドロキシ酸、モノマーのヒドロ キシ酸のラクチド、モノマーのヒドロキシ酸の乳酸ラクチル非環状ダイマーおよ び450までの分子量を有する七ツマーヒドロキシ酸のその他のオリゴマーであ る。Also, films outside these ranges are cloudy and/or brittle. for example, Polymer films with a fraction in excess of 97% S-carbon atoms are Substantially crystalline after heat treatment as in manufacture. Crystallization is in film form performance, optical clarity of films formed from crystalline polymers, and For the production of well-oriented films formed by stretching from reamers. Harmful. Crystalline polymer films are also better than amorphous polymer films. It's also fragile. Reduce the negative effects of highly crystalline polymers on film properties The method involves incorporating chemical species of monomers and low molecular weight oligomers into a polymer matrix. plasticizing the polymer by incorporating and dispersing it. The port of the present invention Plasticizers for monomeric hydroxy acids, monomeric hydroxy acids, Lactide of hydroxy acids, lactyl lactyl acyclic dimer of monomeric hydroxy acids and and other oligomers of heptameric hydroxy acids with molecular weights up to 450. Ru.
ポリヒドロキシ酸中の過剰濃度の可塑剤は、不均一な厚さのフィルムを生じさせ ることがわかっている。フィルムをドラム上にキャストすることにより作る場合 には、過剰の可塑剤がフィルムから分離し、ドラムにくっついてドラムを汚すか 、またはフィルムをドラムにくっつけさせることもある。Excessive concentration of plasticizer in polyhydroxy acids will result in films of non-uniform thickness. It is known that When the film is made by casting it onto a drum Excess plasticizer will separate from the film and stick to the drum, staining it. , or the film may be stuck to the drum.
このため、最小限の量の可塑剤を含むポリマーを用いることが必要であることが わかっている。本発明にしたがって有用なフィルムを得るために必要な可塑剤の 量は、約0.10から約8重量%まで、好ましくは約0.2から6重量%までで ある。かなり好ましい組成範囲は、約0.2から0.4重量%までの可塑剤であ る。これらの可塑剤レベルは、フィルムを製造するために用いられる原料中のポ リヒドロキシ酸および可塑剤の濃度に基づいており、必ずしも本発明の組成物か ら製造されたフィルム中の可塑剤の濃度に対応していない。For this reason, it is necessary to use polymers containing minimal amounts of plasticizers. know. of plasticizers necessary to obtain films useful in accordance with the present invention. The amount is from about 0.10 to about 8% by weight, preferably from about 0.2 to 6% by weight. be. A highly preferred composition range is about 0.2 to 0.4% by weight plasticizer. Ru. These plasticizer levels depend on the potency in the raw materials used to make the film. based on the concentration of hydroxyacid and plasticizer, and not necessarily the composition of the present invention. does not correspond to the concentration of plasticizer in the film produced.
可塑剤含有量は、応用高分子科学、コーン、パン・デン・バーブ、パン・デ・リ ダーおよびフェイエン、第29巻、4265−4277頁(1984) [Jo urnal of AppliedPolymer 5cience、 Kah n、 Van den Betg、 Van de Ridder andFe 7en、volume 29. pages 4265−4277(1984) コに教示されているラクチド含有量分析法によってめることができる。可塑剤リ ッチ組成物中の可塑剤の濃度を減少することが必要になるならば、分離段階とし てまたはフィルム押し出しの間に脱揮発押出機(devola+ilizing extrudcr)を用いてもよい。Plasticizer content is determined by Applied Polymer Science, Cohn, Pan den Barbe, Pan de Ri Dar and Feyen, Vol. 29, pp. 4265-4277 (1984) [Jo Urnal of Applied Polymer 5science, Kah n, Van den Betg, Van de Ridder and Fe 7en, volume 29. pages 4265-4277 (1984) It can be determined by the lactide content analysis method taught in Ko. plasticizer If it becomes necessary to reduce the concentration of plasticizer in the latch composition, a separation step may be used. or during film extrusion. extrudcr) may also be used.
収縮値はフィルム収縮性能の指標である。収縮値は、1)配向フィルムから、試 料の各辺が機械に平行な方向とフィルムを横切る方向となるように、10cmX 10cmの正方形の試料を切り出し;2)この試料を1分間沸騰水に浸し;3) ボイルしたフィルムの長さと幅を測定して平均し;4)ボイルしたフィルムの平 均の長さと幅を10から引き算し、その差に10を掛は算することによりパーセ ント収縮値を計算する;ことによりまる。例えば、ボイルしたフィルム試料の平 均の長さと幅が6cmであると仮定すると、フィルムの収縮値を(10−6)か ける10、すなわち40%と計算する。Shrinkage value is an indicator of film shrinkage performance. The shrinkage value is 1) from the oriented film, 10cm Cut out a 10 cm square sample; 2) Soak the sample in boiling water for 1 minute; 3) Measure and average the length and width of the boiled film; 4) Measure the length and width of the boiled film; Percentage is calculated by subtracting the average length and width from 10, then multiplying the difference by 10. Calculate the shrinkage value; depending on the case. For example, the flattening of a boiled film sample Assuming that the average length and width are 6 cm, the shrinkage value of the film is (10-6). 10, or 40%.
本発明のポリマー組成物は、配向に先立って約0,05から2mmまでの範囲の 均一な厚みのフィルムに成形される。The polymer compositions of the present invention may have a diameter ranging from about 0.05 to 2 mm prior to orientation. Formed into a film of uniform thickness.
フィルム形成は、溶融押出およびシートキャスティング、ブロー成形、溶媒から の沈殿またはポリマーからフィルムを製造するのによく知られた他の手段によっ て達成することができる。こうして形成されたフィルムは、直接に配向装置に供 給してもよいし、貯蔵のためにスプールに巻くかまたは他の方法で使いよ(集め 次いで加工するか使用してもよい。Film formation is from melt extrusion and sheet casting, blow molding, solvent by precipitation or other means well known for producing films from polymers. can be achieved. The film thus formed is directly fed to an orientation device. may be supplied, wound on spools for storage, or otherwise used (collected). It may then be processed or used.
収縮ラップ用途に有用なポリマーフィルムは、前に議論したポリヒドロキシ酸組 成物フィルムを二輪配向することにより調製できる。二軸配向は、フィルムを、 それが移動する方向(機械方向(MD)と呼ばれる)、およびフィルムの面内に おいて機械方向に対して90度の方向(横方向(TD)として知られる)に沿っ て延伸し、それによってフィルムをフィルムの最初のMDおよびTD力方向寸法 の少なくとも2倍に延ばすことを意味する。本発明の二軸配向は、同時的なMD およびTD延伸、および連続的な延伸を含む。同時二軸配向の1つの方法は、チ ューブ状のフィルムを、そのチューブを機械方向に延伸しながら、ブローさせる 。二軸配向は、フィルム温度をポリヒドロキシ酸のガラス転移温度以上およびそ の融点以下に加熱し維持しながらなされる。ポリヒドロキシ酸のガラス転移温度 は、示差走査熱量計(DSC)により測定される。ガラス転移温度は、可塑剤含 有量が増加するにともなって減少し、0.28重量%の可塑剤を含む組成物に対 しては約60℃であるが、20重量%の可塑剤を含む組成物に対しては40℃に すぎない。高い可塑剤濃度は、それから生じるガラス転移温度が、暖かい気候の 地域での貯蔵および輸送中に予期される温度に近すぎるため、好ましくないこと がわかっている。Polymer films useful for shrink wrap applications include the polyhydroxy acid compositions discussed previously. It can be prepared by two-wheel orientation of a composite film. Biaxial orientation makes the film the direction in which it moves (called the machine direction (MD)), and in the plane of the film. along a direction 90 degrees to the machine direction (known as the transverse direction (TD)) Stretch the film, thereby reducing the initial MD and TD force dimensions of the film. This means extending it to at least twice as long. The biaxial orientation of the present invention is characterized by simultaneous MD and TD stretching, and continuous stretching. One method of simultaneous biaxial orientation is to Blowing a tube-shaped film while stretching the tube in the machine direction . Biaxial orientation increases the film temperature above and below the glass transition temperature of the polyhydroxy acid. This is done while heating and maintaining the temperature below the melting point. Glass transition temperature of polyhydroxy acids is measured by differential scanning calorimetry (DSC). The glass transition temperature is decreases with increasing amount of plasticizer, for compositions containing 0.28% by weight of plasticizer. for compositions containing 20% by weight plasticizer, but at 40°C. Only. High plasticizer concentrations result in lower glass transition temperatures in warmer climates. Undesirable as it is too close to the temperatures expected during local storage and transportation I know.
二輪配向したフィルムは、ヒートセツティングにより非収縮性にすることもでき る。ヒートセツティングは、配向したポリマーフィルムを、そのフィルムを拘束 しながら、ポリヒドロキシ酸のガラス転移温度以上であるがその融点以下の温度 にさらすことによりなされる。有効であるとわかっているヒートセツティングの 継続時間は、約1から120秒まで好ましくは約1から80秒までである。本発 明の「非収縮性」の製品は、沸騰水中に1分間浸漬したときに5%以上収縮しな いフィルムと定義される。非収縮性の劣化性のフィルムは、例えば、マイクロ波 で調理可能な食品包装、ゴミ袋および廃棄物コンテナの内張の製造にを用である 。Two-wheel oriented films can also be made non-shrinkable by heat setting. Ru. Heat setting is the process of constraining the oriented polymer film. while the temperature is above the glass transition temperature of the polyhydroxy acid but below its melting point. This is done by exposing it to. Heat settings known to be effective The duration is from about 1 to 120 seconds, preferably from about 1 to 80 seconds. Main departure Ming's "non-shrinkable" products do not shrink by more than 5% when immersed in boiling water for 1 minute. Defined as an ugly film. Non-shrinkable degradable films can be made by e.g. Used in the production of ready-to-cook food packaging, garbage bags and waste container linings. .
実施例 本発明は、ある種の好ましい態様である以下の代表的な例によって示され、ここ で全ての部、割合、およびパーセンテージは、他に示されていなければ、重量に よる。Sl単位以外の重量および寸法の全ての単位は、SI単位に変換されてい る。Example The invention is illustrated by the following representative examples of certain preferred embodiments, and in which: All parts, proportions, and percentages are by weight unless otherwise indicated. evening. All units of weight and dimensions other than SI units have been converted to SI units. Ru.
例1 85%より多いS−および15%より少ないR−不斉炭素を含み、約275.0 00の分子量を有し、ラクチド含有量分析によりめた0、4%より少ない可塑剤 を含む、ポリヒドロキシ酸組成物を、脱揮発部(deyolajilixili on po目)および2.5mmのダイギャップを有する25cm幅の垂直ダイ を備えた、28mmのワーナーーフライデレル(Werner−Pfleide rer)ツインスクリュー押出機によって、約0.03および0.23mmの厚 さのフィルムに押し出す。これらのフィルムを、20℃に維持した、25cm径 のクロムめっきされた冷却ロール上に分離する。両方のフィルムは、弱く脆い。Example 1 Contains more than 85% S- and less than 15% R-asymmetric carbons, about 275.0 Plasticizer with a molecular weight of 0.00 and less than 0.4% as determined by lactide content analysis The polyhydroxy acid composition comprising: 25cm wide vertical die with 2.5mm die gap 28mm Werner-Pfleide with 0.03 and 0.23 mm thickness by twin screw extruder Extrude onto a thin film. These films were prepared at 25 cm diameter, maintained at 20°C. Separate on a chrome-plated cooling roll. Both films are weak and brittle.
0.23mmの厚さのフィルムを、ティー・エムφロング社(T、 M、 Lo ng Co、 、 Inc)のフィルム延伸機を用い、65℃で、最初の幅およ び長さの3倍まで延伸することにより、二軸配向する。配向フィルムは、強く、 堅く、光学的に透明で光沢があり、66%という良好な収縮性フィルム製品の収 縮値を有している。配向フィルムを、拘束下に置き、130℃で1分間ヒートセ ットする。このフィルムは、強く柔軟であり、非収縮性フィルム製品に好都合な 4%という収縮値を有している。A film with a thickness of 0.23 mm was manufactured by T.M.φLong Co., Ltd. (T, M, Lo The initial width and The film is biaxially oriented by stretching it to three times its length. The oriented film is strongly Stiff, optically clear and glossy with good shrink film product yield of 66% It has a reduced value. Place the oriented film under restraint and heat set at 130°C for 1 minute. cut. This film is strong and flexible, making it convenient for non-shrink film products. It has a shrinkage value of 4%.
例2 ヒートセツティングに先立って、例1の二軸配向フィルムの試料を、幅7.6c m、長さ12.7cm、高さ0.64cmの紙のパッドの周りに包み、両面接着 テープでそこに保持する。包んだパッケージを、加熱空気対流オーブン中に、1 00℃で1分間置く。フィルムはパッドの周りで均一に収縮し、光学的に透明で 光沢がある。室温での15か月間の貯蔵の後、フィルムの劣化は観測されず、こ のことはその収縮ラップ用途における有用性を示している。Example 2 Prior to heat setting, a sample of the biaxially oriented film of Example 1 was prepared with a width of 7.6 cm. m, wrapped around a paper pad measuring 12.7 cm long and 0.64 cm high, adhesive on both sides. Hold it there with tape. Place the wrapped package in a heated air convection oven for 1 Leave at 00°C for 1 minute. The film shrinks uniformly around the pad and is optically clear. Shiny. After storage for 15 months at room temperature, no deterioration of the film was observed; This indicates its usefulness in shrink wrap applications.
一方、85%より多いS−および15%より少ないR−不斉炭素原子を含み、ラ クチド含有量分析によりめた20%可塑剤を有するポリヒドロキシ酸組成物を、 例1の方法により0.23mmの厚さを有するフィルムに押し出す。数分間の操 作の後、冷却ロールの表面は可塑剤で被覆され、この可塑剤はロールの伝熱効率 を減少させてフィルムに不均一な厚さと光学的に劣った(すなわちおよそ15か ら40cm2までの大きさの範囲の曇った斑点を有する)フィルム表面をもたら し、このことは最初のポリマー中の可塑剤の量が多すぎたことを示している。On the other hand, it contains more than 85% S- and less than 15% R-asymmetric carbon atoms; A polyhydroxy acid composition with 20% plasticizer determined by cutide content analysis, Extrude according to the method of Example 1 into a film having a thickness of 0.23 mm. several minutes of operation After production, the surface of the cooling roll is coated with a plasticizer, which improves the heat transfer efficiency of the roll. Reduced film thickness and optically poor quality (i.e. approximately 15%) yielding a film surface with cloudy spots ranging in size from up to 40 cm2). However, this indicates that the amount of plasticizer in the initial polymer was too high.
このフィルムを、ティー・エムーロング社のフィルム延伸機を用い、46℃で、 最初の幅および長さの3倍まで延伸することにより、二軸配向する。室温でゆっ くりと収縮する傾向がある、好ましくない柔らかくて曇ったフィルムが生じる。This film was stretched at 46°C using a film stretching machine manufactured by TM Long Co., Ltd. Biaxial orientation is achieved by stretching to three times the original width and length. At room temperature An undesirable soft, cloudy film is produced which has a tendency to shrink.
例3 97%よりいくぶん少ないS−および3%より多いR−不斉炭素原子を含み、約 250,000−300,000の分子量およびラクチド含有量分析によりめた 約5%の可塑剤を有するポリヒドロキシ酸組成物を、例1の方法により、光学的 に透明な、1.5mm厚さのフィルムに押し出す。このフィルムを、例1の方法 により二輪配向して、71%という収縮値を有する、光学的に透明なフィルムを 製造する。一方、97%よりいくぶん多いS−および3%より少ないR−不斉炭 素原子を含み、約300,000の分子量およびラクチド含有量分析によりめた 約6%の可塑剤を有するポリヒドロキシ酸組成物を、1.5mm厚さのフィルム に押し出すと、曇っている。このフィルムを、例1に記載された方法により二輪 配向して、フィルムを製造すると、室温で6か月のエージング後には脆くなり、 このことはこのフィルムを多くの商業的な包装用途に使用するには適さないもの にさせる。Example 3 Containing somewhat less than 97% S- and more than 3% R-asymmetric carbon atoms, about Determined by molecular weight and lactide content analysis of 250,000-300,000 A polyhydroxy acid composition having about 5% plasticizer was optically processed by the method of Example 1. extruded into a transparent, 1.5 mm thick film. This film was prepared using the method of Example 1. to produce an optically clear film with a shrinkage value of 71%. Manufacture. On the other hand, somewhat more than 97% S- and less than 3% R-asymmetric carbon Contains elementary atoms, determined by molecular weight and lactide content analysis of approximately 300,000 A polyhydroxy acid composition having about 6% plasticizer was applied to a 1.5 mm thick film. When I push it out, it's cloudy. This film was applied to two wheels by the method described in Example 1. Oriented to produce a film, it becomes brittle after six months of aging at room temperature; This makes the film unsuitable for use in many commercial packaging applications. Let it be.
要 約 書 本発明は、均一な組成物を得るために材料を溶融処理し、組成物をフィルムに成 形し、およびフィルムを二輪配向することを含む、ポリヒドロキシ酸および可塑 剤からなる劣化性、収縮性のフィルムを製造する方法に関する。また、フィルム を拘束下に維持しながら、二軸配向フィルムを組成物のガラス転移温度より高く その融点より低い温度でヒートセツティングすることにより、非収縮性フィルム が製造される。こうして製造されたフィルムは、使い捨てでき環境的に優しい包 装および他の通常のフィルム用途に有用である。Summary book The present invention involves melt processing materials to obtain a uniform composition and forming the composition into a film. Polyhydroxy acids and plasticizers, including shaping and orienting films The present invention relates to a method for producing a degradable, shrinkable film made of a degradable and shrinkable film. Also, film The biaxially oriented film is heated above the glass transition temperature of the composition while maintaining the By heat setting at a temperature below its melting point, a non-shrinkable film is manufactured. The films produced in this way can be used in disposable, environmentally friendly packaging. Useful for packaging and other conventional film applications.
国際調査報告international search report
Claims (9)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/552,551 US5076983A (en) | 1990-07-16 | 1990-07-16 | Polyhydroxy acid films |
| US552,551 | 1990-07-16 | ||
| PCT/US1991/004307 WO1992001548A1 (en) | 1990-07-16 | 1991-06-25 | Polyhydroxy acid films |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05508819A true JPH05508819A (en) | 1993-12-09 |
| JP2945758B2 JP2945758B2 (en) | 1999-09-06 |
Family
ID=24205821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3512895A Expired - Lifetime JP2945758B2 (en) | 1990-07-16 | 1991-06-25 | Polyhydroxy acid film |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5076983A (en) |
| EP (1) | EP0544701B1 (en) |
| JP (1) | JP2945758B2 (en) |
| AU (1) | AU8289691A (en) |
| IE (1) | IE912457A1 (en) |
| MX (1) | MX9100213A (en) |
| NZ (1) | NZ238942A (en) |
| WO (1) | WO1992001548A1 (en) |
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| JPH09187863A (en) * | 1996-01-11 | 1997-07-22 | Mitsubishi Plastics Ind Ltd | Heat-shrinkable polylactic acid film and method for producing the same |
| JP2003002984A (en) * | 2002-06-14 | 2003-01-08 | Mitsubishi Plastics Ind Ltd | Polylactic acid based film |
| WO2008035762A1 (en) | 2006-09-21 | 2008-03-27 | Asahi Kasei Home Products Corporation | Process for the production of polylactic acid film |
| JP2019131720A (en) * | 2018-01-31 | 2019-08-08 | 大阪瓦斯株式会社 | Plasticizer and resin composition containing the same |
| WO2024203640A1 (en) * | 2023-03-24 | 2024-10-03 | 株式会社カネカ | Method for producing stretched film |
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-
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-
1991
- 1991-06-25 EP EP91913883A patent/EP0544701B1/en not_active Expired - Lifetime
- 1991-06-25 AU AU82896/91A patent/AU8289691A/en not_active Abandoned
- 1991-06-25 WO PCT/US1991/004307 patent/WO1992001548A1/en not_active Ceased
- 1991-06-25 JP JP3512895A patent/JP2945758B2/en not_active Expired - Lifetime
- 1991-07-12 NZ NZ238942A patent/NZ238942A/en unknown
- 1991-07-15 MX MX9100213A patent/MX9100213A/en unknown
- 1991-07-15 IE IE245791A patent/IE912457A1/en unknown
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07207041A (en) * | 1994-01-11 | 1995-08-08 | Mitsubishi Plastics Ind Ltd | Polylactic acid film |
| JPH07205278A (en) * | 1994-01-11 | 1995-08-08 | Mitsubishi Plastics Ind Ltd | Method for producing stretched film of polylactic acid polymer |
| JPH07256753A (en) * | 1994-03-28 | 1995-10-09 | Mitsubishi Plastics Ind Ltd | Heat-shrinkable polylactic acid film |
| JPH09187863A (en) * | 1996-01-11 | 1997-07-22 | Mitsubishi Plastics Ind Ltd | Heat-shrinkable polylactic acid film and method for producing the same |
| JP2003002984A (en) * | 2002-06-14 | 2003-01-08 | Mitsubishi Plastics Ind Ltd | Polylactic acid based film |
| WO2008035762A1 (en) | 2006-09-21 | 2008-03-27 | Asahi Kasei Home Products Corporation | Process for the production of polylactic acid film |
| JP2019131720A (en) * | 2018-01-31 | 2019-08-08 | 大阪瓦斯株式会社 | Plasticizer and resin composition containing the same |
| WO2024203640A1 (en) * | 2023-03-24 | 2024-10-03 | 株式会社カネカ | Method for producing stretched film |
Also Published As
| Publication number | Publication date |
|---|---|
| MX9100213A (en) | 1992-02-28 |
| IE912457A1 (en) | 1992-01-29 |
| EP0544701A1 (en) | 1993-06-09 |
| AU8289691A (en) | 1992-02-18 |
| JP2945758B2 (en) | 1999-09-06 |
| NZ238942A (en) | 1993-03-26 |
| EP0544701B1 (en) | 2002-09-11 |
| WO1992001548A1 (en) | 1992-02-06 |
| EP0544701A4 (en) | 1993-07-14 |
| US5076983A (en) | 1991-12-31 |
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